CA2463777A1 - Fuel cell-use carbon fiber woven fabric, electrode element, fuel cell, mobile unit, and production method for fuel cell-use carbon fiber woven fabric - Google Patents
Fuel cell-use carbon fiber woven fabric, electrode element, fuel cell, mobile unit, and production method for fuel cell-use carbon fiber woven fabric Download PDFInfo
- Publication number
- CA2463777A1 CA2463777A1 CA002463777A CA2463777A CA2463777A1 CA 2463777 A1 CA2463777 A1 CA 2463777A1 CA 002463777 A CA002463777 A CA 002463777A CA 2463777 A CA2463777 A CA 2463777A CA 2463777 A1 CA2463777 A1 CA 2463777A1
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- Canada
- Prior art keywords
- woven fabric
- fuel cell
- carbon fiber
- fiber woven
- carbon
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 239000002759 woven fabric Substances 0.000 title claims abstract description 213
- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 128
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 128
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 111
- 239000000446 fuel Substances 0.000 title claims abstract description 97
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- -1 electrode element Substances 0.000 title description 5
- 230000006835 compression Effects 0.000 claims abstract description 24
- 238000007906 compression Methods 0.000 claims abstract description 24
- 238000009792 diffusion process Methods 0.000 claims abstract description 23
- 239000000835 fiber Substances 0.000 claims description 47
- 229920006286 oxidized acrylic fiber Polymers 0.000 claims description 24
- 239000003054 catalyst Substances 0.000 claims description 16
- 239000007833 carbon precursor Substances 0.000 claims description 15
- 239000006229 carbon black Substances 0.000 claims description 11
- 239000012528 membrane Substances 0.000 claims description 7
- 125000004430 oxygen atom Chemical group O* 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 239000002243 precursor Substances 0.000 claims description 6
- 239000005518 polymer electrolyte Substances 0.000 claims description 5
- 239000005871 repellent Substances 0.000 claims description 5
- 238000010000 carbonizing Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 2
- 241001089723 Metaphycus omega Species 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 28
- 229910052799 carbon Inorganic materials 0.000 description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 238000000034 method Methods 0.000 description 16
- 238000009941 weaving Methods 0.000 description 16
- 230000000052 comparative effect Effects 0.000 description 13
- 238000003763 carbonization Methods 0.000 description 11
- 239000004744 fabric Substances 0.000 description 9
- 230000035699 permeability Effects 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000012298 atmosphere Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 229920005989 resin Polymers 0.000 description 7
- 239000011347 resin Substances 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 229910021397 glassy carbon Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000123 paper Substances 0.000 description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 description 3
- 239000008213 purified water Substances 0.000 description 3
- 239000005060 rubber Substances 0.000 description 3
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 2
- 229920000557 Nafion® Polymers 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 229920000297 Rayon Polymers 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011889 copper foil Substances 0.000 description 2
- 239000010408 film Substances 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 239000002964 rayon Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- FPJNQQRSBJPGHM-UHFFFAOYSA-N 1-chloro-2-nitropropane Chemical compound ClCC(C)[N+]([O-])=O FPJNQQRSBJPGHM-UHFFFAOYSA-N 0.000 description 1
- 229920000298 Cellophane Polymers 0.000 description 1
- PMVSDNDAUGGCCE-TYYBGVCCSA-L Ferrous fumarate Chemical compound [Fe+2].[O-]C(=O)\C=C\C([O-])=O PMVSDNDAUGGCCE-TYYBGVCCSA-L 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- VJYFKVYYMZPMAB-UHFFFAOYSA-N ethoprophos Chemical group CCCSP(=O)(OCC)SCCC VJYFKVYYMZPMAB-UHFFFAOYSA-N 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000002210 silicon-based material Substances 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000007779 soft material Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 238000009864 tensile test Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/023—Porous and characterised by the material
- H01M8/0234—Carbonaceous material
-
- D—TEXTILES; PAPER
- D03—WEAVING
- D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
- D03D15/00—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used
- D03D15/20—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads
- D03D15/242—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads inorganic, e.g. basalt
- D03D15/275—Carbon fibres
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/8605—Porous electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
- H01M4/8817—Treatment of supports before application of the catalytic active composition
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/96—Carbon-based electrodes
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2101/00—Inorganic fibres
- D10B2101/10—Inorganic fibres based on non-oxides other than metals
- D10B2101/12—Carbon; Pitch
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2201/00—Cellulose-based fibres, e.g. vegetable fibres
- D10B2201/20—Cellulose-derived artificial fibres
- D10B2201/22—Cellulose-derived artificial fibres made from cellulose solutions
- D10B2201/24—Viscose
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2321/00—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D10B2321/04—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polymers of halogenated hydrocarbons
- D10B2321/042—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polymers of halogenated hydrocarbons polymers of fluorinated hydrocarbons, e.g. polytetrafluoroethene [PTFE]
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2321/00—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D10B2321/10—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polymers of unsaturated nitriles, e.g. polyacrylonitrile, polyvinylidene cyanide
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2401/00—Physical properties
- D10B2401/02—Moisture-responsive characteristics
- D10B2401/022—Moisture-responsive characteristics hydrophylic
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/20—Fuel cells in motive systems, e.g. vehicle, ship, plane
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T90/00—Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02T90/40—Application of hydrogen technology to transportation, e.g. using fuel cells
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Textile Engineering (AREA)
- Composite Materials (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Inert Electrodes (AREA)
Abstract
A fuel cell-use carbon fiber woven fabric, especially a carbon fiber woven fabric preferably used for the electrode diffusion layer of an electrode element in a fuel cell. The electrode diffusion layer of an electrode elemen t in a fuel cell, requiring conductivity, gas diffusing/permeating features, a nd strength that withstands handling, is formed from carbon fiber woven fabrics as is widely known. The conventional carbon fiber woven fabric poses such problems that deformation by compression is large, the dimension of a fuel cell is significantly changed by pressurizing, irregularities by weave textu re are large, and contact resistance is large. A carbon fiber woven fabric used for a fuel cell-use carbon fiber woven fabric has an average size of warps a nd wefts constituting the woven fabric of 0.005-0.028 g/m, and a woven density of the warps and/or wefts of 20 pieces/cm.
Description
SPECIFICATION
FUEL CELL-USE CARBON FIBER WOVEN FABRIC, ELECTRODE ELEMENT, FUEL
CELL , MOBILE UNIT , AND PRODUCTION METHOD FOR FUEL CELL-USE CARBON
s FIBER WOVEN FABRIC
TECHNICAL FIELD
The present invention relates to a carbon fiber woven fabric to be used in a fuel cell, an electrode element using the carbon fiber woven fabric, a fuel cell using the electrode element, a mobile unit using the fuel cell, and a method for producing a carbon fiber woven fabric to be used in the fuel cell. The invention especially relates to a dense and thin carbon fiber woven fabric to be used in a fuel cell, which can be preferably used as the ~s electrode diffusion layer of an electrode element in a solid polymer electrolyte fuel cell.
BACKGROUND ART
An electrode diffusion layer of a fuel cell is required to zo allow diffusion and permeation of substances participating in current collecting function and electrode reaction. Furthermore, a material constituting the electrode diffusion layer is required to have electric conductivity, gas diffusibility, gas permeability, strength to endure handling, etc.
zs As the material used to form the electrode diffusion layer of a fuel cell, a porous carbon plate comprising short carbon i fibers bound with carbon, described in JP-06-20710-A, JP-07-326362-A or JP-07-220735-A, is known. However, the porous carbon plate has such problems that it is difficult to produce the plate in a continuous longer form and that the carbon used s as a binder is likely to be destroyed under the pressure acting when the electrode is produced or when the carbon plate is assembled into a cell.
As a material capable of being formed as a continuously long material to be used for forming an electrode diffusion layer, a carbon fiber woven fabric is known. Examples of the carbon fiber woven fabric include "PANEX PWB-3" produced by Stackpole Fibers Company which is described in US-4,293,396-A and "AVCARB"
produced by Textron Specialty Materials which is described in JP-10-261421-A.
~s The "PANEX PWB-3" can provide a continuously long material, but if the carbon fiber woven fabric is used as an electrode diffusion layer, it has such problems that a dimension of fuel cell is greatly changed under pressurization, and that separator grooves are filled with the woven fabric, since the woven fabric zo is greatly deformed under compression. Furthermore, it has a problem that since it is difficult to apply a catalyst layer because of the large undulation attributable to its weave texture, the contact resistance becomes large. Moreover, it has a problem that a woven fabric formed of thick weaving yarns but having a zs low unit weight causes the catalyst layer to come off , since the gaps between fibers are large.
FUEL CELL-USE CARBON FIBER WOVEN FABRIC, ELECTRODE ELEMENT, FUEL
CELL , MOBILE UNIT , AND PRODUCTION METHOD FOR FUEL CELL-USE CARBON
s FIBER WOVEN FABRIC
TECHNICAL FIELD
The present invention relates to a carbon fiber woven fabric to be used in a fuel cell, an electrode element using the carbon fiber woven fabric, a fuel cell using the electrode element, a mobile unit using the fuel cell, and a method for producing a carbon fiber woven fabric to be used in the fuel cell. The invention especially relates to a dense and thin carbon fiber woven fabric to be used in a fuel cell, which can be preferably used as the ~s electrode diffusion layer of an electrode element in a solid polymer electrolyte fuel cell.
BACKGROUND ART
An electrode diffusion layer of a fuel cell is required to zo allow diffusion and permeation of substances participating in current collecting function and electrode reaction. Furthermore, a material constituting the electrode diffusion layer is required to have electric conductivity, gas diffusibility, gas permeability, strength to endure handling, etc.
zs As the material used to form the electrode diffusion layer of a fuel cell, a porous carbon plate comprising short carbon i fibers bound with carbon, described in JP-06-20710-A, JP-07-326362-A or JP-07-220735-A, is known. However, the porous carbon plate has such problems that it is difficult to produce the plate in a continuous longer form and that the carbon used s as a binder is likely to be destroyed under the pressure acting when the electrode is produced or when the carbon plate is assembled into a cell.
As a material capable of being formed as a continuously long material to be used for forming an electrode diffusion layer, a carbon fiber woven fabric is known. Examples of the carbon fiber woven fabric include "PANEX PWB-3" produced by Stackpole Fibers Company which is described in US-4,293,396-A and "AVCARB"
produced by Textron Specialty Materials which is described in JP-10-261421-A.
~s The "PANEX PWB-3" can provide a continuously long material, but if the carbon fiber woven fabric is used as an electrode diffusion layer, it has such problems that a dimension of fuel cell is greatly changed under pressurization, and that separator grooves are filled with the woven fabric, since the woven fabric zo is greatly deformed under compression. Furthermore, it has a problem that since it is difficult to apply a catalyst layer because of the large undulation attributable to its weave texture, the contact resistance becomes large. Moreover, it has a problem that a woven fabric formed of thick weaving yarns but having a zs low unit weight causes the catalyst layer to come off , since the gaps between fibers are large.
The invention has been completed in view of the above-mentioned problems of the prior art. An object of the invention is to provide a thin carbon fiber woven fabric slightly deformable under compression, small in electric resistance and s suitable for use as an electrode diffusion layer in a fuel cell.
Another object of the invention is to provide an electrode element using a carbon fiber woven fabric to be used in a fuel cell of the invention, a fuel cell using the electrode element, and a mobile unit using the fuel cell. A further object of the invention is to provide a method for producing a carbon fiber woven fabric to be used in a fuel cell of the invention.
DISCLOSURE OF THE INVENTION
A carbon fiber woven fabric for a fuel cell of the invention ~s is characterized in that the average fineness of the warp yarns and the weft yarns constituting the woven fabric is in the range of 0.005 to 0. 028 g/m, and that the weave density of the warp yarns and/or the weft yarns is not less than 20 yarns/cm.
It is preferred that the unit weight of the woven fabric zo is in the range of 50 to 150 g/mz .
It is preferred that the thickness of the woven fabric is in the range of 0.1 to 0.3 mm.
It is preferred that the value of N x W is not less than 0 . 6 where N (yarns/cm) is the weave density of the warp yarns and/or zs weft yarns and W (cm/yarn) is the yarn width.
It is preferred that the crush value the woven fabric under compression is not more than 0.15 mm.
It is preferred that the warp yarns and/or the weft yarns are spun yarns.
It is preferred that the electric resistance of the woven s fabric is not more than 30 mS2cm2, and that the differential pressure caused when 14 cm3/cm2/sec of air is passed through the woven fabric in the thickness direction is not more than 5 mm Aq.
It is preferred that the ratio of the number of oxygen atoms to the number of carbon atoms on the carbon fiber surfaces of the woven fabric is not less than 0.06 and less than 0.17.
It is preferred that the woven fabric contains carbon black on its surfaces and/or inside.
It is preferred that the woven fabric contains a water-repellent substance.
~s An electrode element for a fuel cell of the invention is formed of the above-mentioned carbon fiber woven fabric for a fuel cell of the invention.
It is preferred that the electrode element comprises an electrode diffusion layer formed of the above-mentioned carbon Zo fiber woven fabric for a fuel cell of the invention.
It is preferred that the electrode diffusion layer has a catalyst layer disposed thereon in layer.
It is preferred that the electrode diffusion layer has a catalyst layer and a polymer electrolyte film deposited thereon is in layers.
A fuel cell of the invention comprises the above-mentioned electrode element of the invention.
It is preferred that the fuel cell has a grooved separator provided on the electrode element.
A mobile unit of the invention is mounted with the s above-mentioned fuel cell.
A method for producing a carbon fiber woven fabric for a fuel cell of the invention comprises a pressurization step of pressurizing a precursor fiber woven fabric composed of carbon precursor fibers in the thickness direction and a step of carbonizing the precursor fiber woven fabric.
In the method for producing a carbon fiber woven fabric for a fuel cell, it is preferred that the pressurization step is carried out at a heating temperature of not more than 300°C at a pressure of 5 to 500 kg/cm.
~s In the method for producing a carbon fiber woven fabric for a fuel cell, it is preferred that the carbon precursor fibers are oxidized acrylic fibers.
THE BEST MODES FOR CARRYING OUT THE INVENTION
Zo In the carbon fiber woven fabric for a fuel cell of the invention, it is necessary that the average fineness of the warp yarns and the weft yarns constituting the woven fabric is in the range of 0.005 to 0.028 g/m. It is preferable that the average fineness is in the range of 0.01 to 0. 026 g/m, and more preferably zs in the range of 0.013 to 0.022 g/m. An average fineness of more than 0.028 g/m is not preferred, since the woven fabric becomes thick or a space between weaving yarns becomes large.
If the unit weight of a woven fabric is A ( g/m2 ) , the density of warp yarns is Nw (yarns/cm) , and the density of weft yarns is Nf ( yarns / cm ) , then the average f inenes s can be obtained from the s following equation (I).
Average fineness ( g/m ) - A/ ( Nw + Nf ) / 100 ... ( I ) In the carbon fiber woven fabric for a fuel cell of the invention, it is necessary that the weave density of the warp yarns and/or the weft yarns is not less than 20 yarns/cm.
It is preferable that the weave density is not less than 22 yarns/cm. If the weave density is too low, the spaces between weaving yarns become large, and such problems are likely to occur that the catalyst layer is likely to come off , and that since the electrolytic membrane is likely to dry, high cell characteristics ~s cannot be obtained. It is especially preferable that both the warp yarns and the weft yarns have the weave density mentioned above . If the weave density increases , the weaving speed declines to raise the cost. It is, therefore, preferable that the weave density is not more than 35 yarns/cm, and more preferably not more Zo than 30 yarns/cm.
In the measurements of the average fineness and the weave density, in the case where the warp yarns and the weft yarns cannot be identified which is which in the woven fabric, the yarns in a given direction should be considered as warp yarns , and the yarns is in the other direction, as weft yarns.
It is preferred that the unit weight of the carbon fiber woven fabric for a fuel cell of the invention is in the range of 50 to 150 g/m2. A more preferred range is from 70 to 120 g/m2, and a further more preferred range is from 80 to 98 g/m2.
In the case where the unit weight is too low, the spaces s between the weaving yarns constituting the woven fabric are so large that there occur such problems that the catalyst layer comes off and that since the electrolytic membrane is likely to dry, high cell characteristics cannot be obtained. In the case where the unit weight is too high, it is difficult to produce the woven ~o fabric, and the woven fabric tends to be thick. As a result, such problems are likely to occur that the fuel cell is dimensionally greatly changed under pressurization, and that the separator grooves are likely to be filled with the woven fabric. In the case where the woven fabric has carbon black, resin and the like is deposited, the weight excluding these deposits should be the weight of the carbon fiber woven fabric.
It is preferred that the thickness of the carbon fiber woven fabric for a fuel cell of the invention is in the range of 0.1 to 0.3 mm. A more preferred range is from 0.13 to 0.25 mm, and zo a further more preferred range is from 0 . 15 to 0 . 20 . The thickness refers to the thickness measured when a pressure of 0.15 MPa is applied to the carbon fiber woven fabric.
In the case where the thickness is too small , such a problem occurs that since the electrolytic membrane is likely to dry, high zs cell characteristics cannot be obtained. Furthermore, in the case where the thickness is too large, such problems are likely to occur that the fuel cell is dimensionally greatly changed under pressurization, and that the separator grooves are likely to be filled with the woven fabric.
If the weave density of the warp yarns and/or the weft yarns s of the carbon fiber woven fabric for a fuel cell of the invention is N (yarns/cm) and the yarn width is W (cm/yarn), then it is preferred that the value of product N x W is not less than 0.6.
More preferred is not less than 0 . 65 , and further more preferred is not less than 0.7.
The yarn width W refers to the width viewed in the direction perpendicular to the face of the woven fabric. The yarn width W can also be measured with the woven fabric magnified as an SEM
photograph, etc. It is preferred that the N x W values of both the warp yarns and the weft yarns are not less than 0.6 ~s respectively.
In the case where the warp yarns cannot be distinguished from the weft yarns on the woven fabric as explained in the above, the yarns in a given direction should be warp yarns , and the yarns in the other direction, weft yarns.
zo In the case where the value of N x W is too small, there occur such problems that since the spaces between weave yarns are large, the catalyst layer comes off, that since the surface is rough, the contact between the catalyst layer and the separator is not sufficient, and that since the electrolytic membrane is zs likely to dry, high cell characteristics cannot be obtained. It is preferred that the value of N x W is not more than 0.96. More a preferred is not more than 0.90, and further more preferred is not more than 0.85. If the value of N x W is too high, weaving is so difficult as to lower the weaving speed, hence increasing the cost.
s It is preferred that the crush value of the carbon fiber woven fabric for a fuel cell of the invention under compression is not more than 0.15 mm. More preferred is not more than 0.12 mm, and further more preferred is not more than 0.10 mm.
The crush value under compression refers to the difference between the thickness measured at a pressure of 0.15 MPa and the thickness measured at a pressure of 1.5 MPa. In the case where the crush value under compression is too large, there occur such problems that stack clamping is difficult, that it is difficult to achieve a uniform height, and that the woven fabric fills the is separator grooves.
It is preferred that the warp yarns and/or the weft yarns constituting the carbon fiber woven fabric of the invention are spun yarns . Since spun yarns have many voids in them, higher air permeability and higher water permeability can be obtained.
zo It is preferred that the electric resistance of the carbon fiber woven fabric for a fuel cell of the invention is not more than 30 mSZcm2. More preferred is not more than 25 mSZcm2, and further more preferred is not more than 20 m52cm2. If the electric resistance is too high, the woven fabric used in an electrode of zs a fuel cell increases the voltage loss.
The method for measuring electric resistance is as follows .
Two plates each of which is a vitreous carbon plate overlaid with a copper foil, wherein the vitreous carbon plate has the width of 50 mm, length of 200 mm, thickness of 1. 5 mm and a smooth surface, and the copper foil has the width of 50 mm, length of 200 mm and s thickness of 0.1 mm are prepared. The plates are called test electrodes . The two test electrodes are overlaid on each other with the vitreous carbon sheets facing each other, to cross each other at their central portions . The carbon fiber woven fabrics are cut to have area S ( cmz ) , and the cut carbon fiber woven fabrics are pressurized to apply a pressure of 0.98 MPa for the area of the fabrics . At the ends on one side of the two test electrodes , current terminals are installed, and at the ends on the other side, voltage terminals are installed. Using the current terminals, a current of 1 A is made to flow between the two test electrodes.
is The voltage V (V) across the voltage terminals is measured, to calculate resistance R (m52cm2 ) from the following equation ( II ) .
R = 1,OOOV x S ... (II) It is preferred that the differential pressure is not more than 5 mm Aq, when 14 cm3/cm2/sec of air is passed in the thickness Zo direction of the carbon fiber woven fabric for a fuel cell of the invention. A more preferred range is from 0.2 to 2 mm Aq, and a further more preferred range is from 0.4 to 1.5 mm Aq. In the case where the differential pressure is too large, the air permeability, hydrogen permeability and water permeability are is low, and the cell voltage tends to be low. In the case where the differential pressure is too small, the water is likely to evaporate, and the resistance of the membrane tends to be higher.
In the case where carbon black, resin and the like are deposited on the woven fabric, these deposits should be removed before measuring the differential pressure.
s It is preferred that the ratio of the number of oxygen atoms to the number of carbon atoms on the surfaces of the carbon fibers constituting the carbon fiber woven fabric for a fuel cell of the invention is not less than 0.06 and less than 0.17. A more preferred range is not less than 0.10 and not more than 0.16, and a further more preferred range is not less than 0.11 and not more than 0.15.
The ratio ( O/C ) of the number of oxygen atoms to the number of carbon atoms on the surfaces of the carbon fibers constituting the carbon fiber woven fabric is defined by the following ~s equation.
O/C = (Rate of oxygen atoms on fiber surfaces)/(Rate of carbon fibers on fiber surfaces) If the ratio O/C on the surfaces of carbon fibers is less than 0.06, the fiber surfaces are low in hydrophilicity, and the ao migration of water in the yarns owing to the capillary tubes formed by plural carbon fibers tends to decrease . As a result , the extra water in the system cannot be efficiently discharged, and the water produced due to the power generation reaction is accumulated to clog the cathode electrode with water with a tendency of zs lowering the gas diffusibility.
If the ratio O/C on the surfaces of carbon fibers is not less than 0.17, the fiber surfaces become too high in hydrophilicity. Therefore, even in the case where the quantity of produced water is small, the cathode electrode can be clogged with water with a tendency of lowering the gas diffusibility. If s the ratio O/C is in the range mentioned above, the surfaces of the fibers constituting the carbon fiber woven fabric for a fuel cell of the invention are moderately hydrophilic. Therefore, the water can highly migrate in the woven fabric owing to the capillary tubes formed by plural carbon fibers, to give a feature that the cathode electrode is unlikely to be clogged with water. For this reason, the extra water in the system can be efficiently discharged, to allow excellent water control.
The ratio of the number of oxygen atoms to the number of carbon atoms on the surfaces of carbon fibers can be measured by ~s X-ray photoelectron spectroscopy.
It is preferred that the carbon fiber woven fabric for a fuel cell of the invention contains carbon black on its surfaces and/or inside for the purposes of increasing electric conductivity, smoothening the surfaces and controlling the water 2o permeability. The method for adding carbon black is not especially limited, but it is preferred that carbon black is bound to the woven fabric using a resin or the like as an adhesive.
It is preferred that the carbon fiber woven fabric for a fuel cell of the invention contains a water-repellent substance 2s for the purpose of preventing clogging with water when it is used in a fuel cell. Furthermore, a water-repellent substance can also be used as an adhesive for the carbon black. The water-repellent substance is not especially limited, and for example, a fluorine-containing compound, silicon-containing compound or the like can be preferably used.
s The method f or producing the carbon f fiber woven f abric f or a fuel cell of the invention is not especially limited. For example, yarns consisting of carbon fibers can be woven to produce a carbon fiber woven fabric, or carbon precursor fibers can also be woven to produce a precursor fiber woven fabric that is then io carbonized into a carbon fiber woven fabric. As another method, a commercially available precursor fiber woven fabric can also be carbonized to produce a carbon fiber woven fabric. In the case where yarns consisting of carbon fibers are woven, it is likely to occur that the carbon fibers are broken or folded. Furthermore, is the warp yarns and the weft yarns are likely to be shifted to deform the meshes of the produced carbon fiber woven fabric, and the warp yarns and the weft yarns at the edges of the woven fabric are likely to come off . Therefore, the latter method of carbonizing a carbon precursor fiber woven fabric is preferred.
Zo The carbon fibers or precursor fibers of carbon fibers used for producing the carbon fiber woven fabric for a fuel cell of the invention are not especially limited. Examples of them include polyacrylonitrile-based carbon fibers, rayon-based carbon fibers, phenol-based carbon fibers, pitch-based carbon zs fibers, oxidized acrylic fibers, rayon fibers, phenol fibers, infusible pitch fibers, etc. An especially preferred method is to carbonize the woven fabric produced by weaving oxidized acrylic ffibers.
In the process for producing the carbon fiber woven fabric for a fuel cell of the invention, it is preferred to include a s step of pressurizing in the thickness direction, the woven fabric produced by weaving carbon precursor fibers , since the crush value under compression can be kept small, for example, when plural electrode diffusion layers formed of carbon fiber woven fabrics are laminated for producing a fuel cell.
It is preferred that the pressurization in the thickness direction is carried out before or during carbonization. The pressurization before or during carbonization is more effective in lessening the crush value under compression than the pressurization after carbonization.
~s The method of pressurizing before carbonization can be a continuous pressurization method using a roll press or belt press or a surface load pressurization method using a batch press or load. In view of the efficiency of the pressurization step, it is preferred to use a roll press or belt press that allows Zo continuous pressurization.
It is preferred that the temperature during pressurization is not more than 300°C. A more preferred range is from 150 to 250°C, and a further more preferred range is from 170 to 230°C.
In the case where the temperature is too low, the deformation under zs compression is too small, and the effect of reducing the thickness cannot be sufficiently obtained. In the case where oxidized acrylic fibers are used, a remarkable pressurization effect can be observed at 150°C or higher. In the case where the temperature is too high, since the oxidation of carbon precursor fibers in air takes place, the pressurization must be carried out in an s inactive atmosphere. Furthermore, because of high temperature, equipment maintenance and process control become difficult . In the case of oxidized acrylic fibers, the problems of oxidation and deterioration do not occur at 250°C or lower, since the fibers underwent flame-retarding treatment.
In the case where the pressurization is carried out using rolls, it is preferred that the surface of at least one of the two rolls used for pressurization is made of a soft material such as rubber, resin, paper or nonwoven fabric for preventing the breaking of carbon precursor fibers and the decline of tensile is strength. It is preferred that the line load of pressurization is in the range of 10 to 500 kg/cm. A more preferred range is from 50 to 300 kg/cm, and a further more preferred range is from 150 to 200 kg/cm.
In the case where hard rolls made of a metal or the like zo are used for pressurization, it is preferred that a clearance of 50 E,im or more is established or that the line load is kept in the range of 5 to 200 kg/cm, for preventing the destruction of the woven fabric, the breaking of the fibers of the woven fabric, and the decline of tensile strength. A more preferred range of line is load is from 10 to 100 kg/cm, and a further more preferred range is from 20 to 70 kg/cm.
In the case where a surface load is used for pressurization, it is preferred that the pressure is 5 MPa or more.
In the case where a woven fabric of carbon precursor fibers is pressurized while being carbonized, it is only required that s the pressurization is carried out at least at any moment in the carbonization step. In the case where preliminary carbonization at the highest temperature of about 500 to 1,000°C is followed by regular carbonization at the highest temperature of higher than 1, 000°C for carrying out carbonization twice , it is preferred that the woven fabric is pressurized during at least either preliminary carbonization or regular carbonization. The method of pressurization can be a continuous pressurization using rolls or belt, or a surface load pressurization, or a method of carbonizing a rolled woven fabric for pressurization using the tension of ~s rolling and the tension caused by the shrinkage during carbonization, though the method is not limited to these methods.
In the case where a rolled woven fabric of carbon precursor fibers is carbonized, it is preferred that the outermost layer of the roll is covered with paper, film or woven fabric with a Zo surface smoother than the woven fabric, since the woven fabric can be carbonized without wrinkling even at the outermost layer.
More particularly it is preferred to cover the woven fabric of carbon precursor fibers with paper, film or woven fabric made of carbon or any other material capable of being carbonized and is incapable of molten when carbonized, such as a polyimide, cellophane or cellulose.
In the case where a woven fabric of carbon precursor fibers is carbonized and subsequently pressurized, it is preferred to pressurize with the woven fabric wetted with a liquid substance such as water or organic solvent, or to pressurize the woven fabric s having a resin such as a fluorine resin deposited. It is more preferred that a carbonized woven fabric having a resin deposited is pressurized at higher than its melting point or thermal deformation temperature.
In the carbon fiber woven fabric for a fuel cell of the invention, the carbon produced when an organic material deposited on the carbon fibers or carbon precursor fibers is carbonized, can also remain deposited. The deposited carbon has an effect of inhibiting the deformation under the pressurization of the carbon fiber woven fabric, but on the other hand, has a problem ~s of lowering the gas permeability and the flexibility of the woven fabric. Therefore, it is preferred that the amount of the carbon is 20 wt~ or less . More preferred is 5 wt~ or less , and further more preferred is 2 wt~ or less.
The carbon fiber woven fabric for a fuel cell of the Zo invention can be preferably used as an electrode component such as a gas diffusion electrode for a fuel cell, since it has electric conductivity and fluid permeability.
Furthermore, the carbon fiber woven fabric for a fuel cell of the invention can be preferably used as a conductive sheet to zs be used in a fuel cell, especially as an electrode diffusion layer of a fuel cell. It can be especially suitably used as an electrode i7 diffusion layer of a fuel cell having a grooved separator. In the case where a grooved separator is used as passages for feeding oxygen and a fuel to a fuel cell electrode, if the crush value of the carbon fiber woven fabric under compression is large, the s portions of the woven fabric facing the grooves and hence not subjected to compression go into the grooves, to inhibit the function as the passages of oxygen and fuel. The carbon fiber woven fabric for a fuel cell of the invention, that is thin in thickness and small in the crush value under compression, can effectively avoid inhibiting the passage function. As a result, the grooves can have a smaller depth and the device can be made more compact.
Moreover, the carbon fiber woven fabric for a fuel cell of the invention can be preferably used as an electrode diffusion is layer having a catalyst layer disposed thereon as a layer or having a catalyst layer and a polymer electrolyte membrane disposed thereon as layers to form a unit. Still furthermore, the electrode diffusion layer or the unit can be preferably used as a component of a fuel cell. The fuel cell containing the carbon zo fiber woven fabric for a fuel cell of the invention, which is flexible and small in the crush value under compression, is strong against vibration and impact, is compact, and is suitable as a fuel cell for a mobile unit . It is especially suitable as a fuel cell for a mobile unit requiring a compact fuel cell, above all, as for a motor vehicle or two-wheeled car.
Examples are described below. The properties described in 1s the examples were measured according to the following methods.
Crush value under compression:
A carbon fiber woven fabric was placed on a smooth table, and a micrometer indenter having a diameter of 5 mm was allowed s to descend from above. With a load applied to the indenter, the thickness was measured at a pressure of 0.15 MPa, and with the load further increased, the thickness was measured at a pressure of 1.5 MPa. The difference between the thickness measured at a pressure of 0.15 MP and the thickness measured at a pressure of 1.5 MPa was identified as the crush value. A smaller crush value is more desirable.
Electric resistance:
The method described before was used to obtain the electric resistance from the following equation. A lower electric is resistance is more desirable.
R = 1,OOOV x S
where R: Resistance (mS2cmz) V: Voltage across voltage terminals (V) S : Area of carbon f fiber woven fabric ( cmz ) zo Voltage at 0 . 7 A/cmz A carbon fiber woven fabric was coated with a mixture consisting of carbon black and polytetrafluoroethylene, and the coated fabric was heat-treated at 380°C, to produce a woven fabric having a carbon layer. The deposited amount of the mixture zs consisting of carbon black and polytetrafluoroethylene was about 2 mg / cmz .
On the other hand, a mixture consisting of platinum-loaded carbon as a catalyst and Nafion was deposited on both sides of Nafion 112 (produced by E. I. du Pont de Nemours and Company), to prepare a membrane-catalyst sheet . The amount of platinum as s a catalyst was about 0.5 mg/cmz.
The membrane-catalyst sheet was held between two carbon-layered woven fabrics having the carbon layers turned inside, and the laminate was heated at 130°C and pressurized at 3 MPa for integration, to obtain a membrane-electrode assembly io ( MEA ) .
The MEA was held between grooved separators , and the cell characteristicswere measured according to a conventional method.
The cell temperature was 70°C, and the temperature at which hydrogen gas was applied was 80°C , while the temperature at which is air was applied was 60°C. The gas pressure was atmospheric pressure. At 0.7 A/cmz, the hydrogen availability was 70~ and the air availability was 40~ . A higher voltage is more desirable .
At 0.7 A/cmz, 0.5 V or higher is acceptable.
Tensile strength:
zo A woven fabric was cut to have a dimension of 5 to 7 cm in the warp direction and a dimension of 1.5 to 1.7 cm in the weft direction. Several warp yarns at both the edges in the weft direction were removed, to ensure that there were no broken warp yarns in the sample having a length of 5 to 7 cm. The width across zs the remaining warp yarns of the sample was measured as a sample width, and a tensile test was carried out at a span of 3 cm and a tensile speed of 1 mm/min . The value obtained by dividing the maximum load ( kg ) by the sample width ( cm ) was identified as the tensile strength.
Examples 1, 2, 3, 4 and 5 s Spun yarns of oxidized acrylic fibers ("Lastan" produced by Asahi Kasei Corp. , 1/34 Nm = 0.029 g/m) were woven into a plain weave. The woven fabric was carbonized in two steps at the highest temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of each oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness, weaving yarn width W and the value of N x W of each carbon fiber woven fabric are shown in Table 1.
Example 6 ~s Spun yarns of oxidized acrylic fibers (produced by Asahi Kasei Corp. , 1/34 Nm = 0.029 g/m) were used as warp yarns and spun yarns of oxidized acrylic fibers (produced by Asahi Kasei Corp. , 2/34 Nm = 0.059 Nm) were used as weft yarns to produce a plain weave. The woven fabric was carbonized in two steps at the highest 2o temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness , weaving yarn width W and the value of N x W of the carbon 2s fiber woven fabric are shown in Table 1.
Example 7 Oxidized acrylic fibers (produced by Toray Industries, Inc . ) were spun into yarns by a draf t zone system spinning . The fineness of the spun yarns was 1/40 Nm = 0.025 g/m. The spun yarns were woven into a plain weave . The woven fabric was carbonized s in two steps at the highest temperatures of 650°C and 1, 950°C
in an inactive atmosphere, to obtain a carbon fiber woven fabric.
The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight , weave densities , average weave density N, fineness, thickness, weaving yarn width W and the value of N x W of the carbon fiber woven fabric are shown in Table 1.
Example 8 The oxidized acrylic fiber woven fabric of Example 1 was held between carbon sheets , carbonized at the highest temperature of 800°C in an inactive atmosphere with a pressure of 2.8 g/cm2 ~s applied to the woven fabric, depressurized and carbonized at 1,950°C, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness, weaving yarn width W and the value of N x zo W of the carbon fiber woven fabric are shown in Table 1.
Example 9 The oxidized acrylic fiber woven fabric of Example 1 was fed through a roll press consisting of one iron roll and one rubber roll ( iron roll 200°C, rubber roll 120°C ) , to be pressurized at 2s 200 kg/cm. The woven fabric was carbonized in two steps at the highest temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness, weaving yarn width W and the value s of N x W of the carbon fiber woven fabric are shown in Table 1.
Examples 10, 11, 12, 13 and 14 The oxidized acrylic fiber woven fabric of Example 5 was fed through a roll press consisting of two iron rolls ( roll temperature 60 , 100 , 125 , 150 or 200°C ) , to be pressurized at 50 kg/cm. The woven fabric was carbonized at the highest temperature of 1,950°C in vacuum, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness and thickness of each carbon fiber woven ~s fabric are shown in Table 1.
Examples 15, 16, 17 and 18 The oxidized acrylic fiber woven fabric of Example 5 was fed through a roll press consisting of two iron rolls (roll temperature 200°C) , to be pressurized at 11, 100, 150 or 250 kg/cm.
2o The woven fabric was carbonized at the highest temperature of 1,950°C in vacuum, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness and thickness of each carbon fiber woven 2s fabric are shown in Table 1.
Example 19 The oxidized acrylic fiber woven fabric of Example 5 was fed through a roll press consisting of two iron rolls (roll temperature 200°C ) having a clearance of 150 Vim, to be pressurized at 250 kg/cm. The woven fabric was carbonized at the highest s temperature of 1, 950°C in vacuum, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight , weave densities , average weave density N, fineness and thickness of the carbon fiber woven fabric are shown in Table 1.
Example 20 In a beaker containing 500 ml of 0 . 1N sulfuric acid, a carbon sheet was used as the cathode, and the carbon fiber woven fabric of Example 4 cut into a size of 8 cm x 8 cm was used as the anode, for carrying out electrolytic treatment with a current of 48 mA
~s kept flowing for 125 seconds. After completion of electrolytic treatment, the carbon fiber woven fabric was washed with purified water, and dried in a 100°C oven for 10 minutes, to obtain a carbon fiber woven fabric treated to be hydrophilic.
Example 21 zo In a beaker containing 500 ml of 0 . 1N sulfuric acid, a carbon sheet was used as the cathode, and the carbon fiber woven fabric of Example 4 cut into a size of 8 cm x 8 cm was used as the anode, for carrying out electrolytic treatment with a current of 48 mA
kept flowing for 250 seconds . After completion of electrolytic zs treatment, the carbon fiber woven fabric was washed with purified water, and dried in a 100°C oven for 10 minutes , to obtain a carbon fiber woven fabric treated to be hydrophilic.
Comparative Example 1 Spun yarns of oxidized acrylic fibers (produced by Asahi Kasei Corp. , 2/34 Nm = 0.059 g/m) were woven into a plain weave.
s The woven fabric was carbonized in two steps at the highest temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness , weaving yarn width W and the value of N x W of the carbon fiber woven fabric are shown in Table 1.
Comparative Example 2 Torayca Cloth (produced by Toray Industries, Inc.) "C06349B" was heated at 1,400°C in an inactive atmosphere, to ~s remove the sizing agent. The unit weight, weave densities, average weave density N, fineness , thickness , weaving yarn width W and the value of N x W of the carbon fiber woven fabric are shown in Table 1.
Comparative Example 3 zo In a beaker containing 500 ml of 0 . 1N sulfuric acid, a carbon sheet was used as the cathode , and the carbon f fiber woven fabric of Example 4 cut into a size of 8 cm x 8 cm was used as the anode, for carrying out electrolytic treatment with a current of 48 mA
kept flowing for 500 seconds . After completion of electrolytic is treatment, the carbon fiber woven fabric was washed with purified water, and dried in a 100°C oven for 10 minutes, to obtain a carbon fiber woven fabric treated to be hydrophilic.
For the carbon fiber woven fabrics obtained in Examples 1 to 21 and Comparative Examples 1 to 3 , the respective values of the crush value under compression, electric resistance, and s differential pressure in air permeation are shown in Table 2, together with the values of the voltage measured with a current of 0.7 A/cmz in the solid polymer electrolyte fuel cells produced using the respective woven fabrics . In the woven fabric of Comparative Example 1, the applied carbon black and polytetrafluoroethylene were separated from the woven fabric, not allow the cell characteristics to be measured.
As can be seen from Tables 1 and 2 , the carbon fiber woven fabrics for a fuel cell of the invention were thin and small in the crush value under compression, showing good cell ~s characteristics. On the other hand, the woven fabrics of Comparative Examples 1 and 2 having an average fineness of more than 0.03 g/m were inferior in cell characteristics. That is, the woven fabric of Comparative Example 1 was relatively thick and large in the crush value under compression. The woven fabric zo of Comparative Example 2 was as low as 0.44 V in voltage.
From the comparison of Examples 5 and 10 to 14, it can be seen that pressing can reduce the thickness, to make the crush value under compression small, and that the effect of thinning at 150°C or higher is remarkable.
zs From the comparison of Examples 5 and 14 through 19 , it can be seen that if the pressure of a roll press consisting of two metallic rolls is raised, the thickness is reduced to make the crush value under compression small. On the other hand, as shown in Table 3, if the pressure is raised especially to 100 kg/cm or higher, it is necessary to establish a clearance between the rolls s and to select an adequate pressure, since otherwise the tensile strength of the woven fabric declines.
As shown in Table 4, since the woven fabrics of Examples 15 and 16 are adequately hydrophilic on the fiber surfaces , their voltages were 0.61 V and 0.62 V respectively, being higher than 0.60 V of Example 4. On the other hand, in Comparative Example 3 , since the ratio O/C was 0 . 17 , the hydrophilicity on the f fiber surfaces was so high that the voltage was as low as 0.41 V.
Table 1 Oxidized Carbon fiber fiber woven woven fabric fabric Weave density weight weight Weave density Warp yarnsWeft yarns Warp yarnsWeft yarns (yarns/cm)(yarns/cm)(g/mZ) (g/mz) (yarns/cm)(yarns/cm) Example 17.0 17.5 104 72 20.0 20.0 Example 24.0 23.0 157 99 28.0 26.0 Example 24.0 17.5 140 88 27.0 20.5 Example 22.0 22.0 150 93 25.5 25.5 Example 22.5 20.0 146 91 25.0 22.5 Example 14.0 18.0 164 102 16.5 20.0 Example 23.0 20.0 126 86 27.0 25.0 Example 17.0 17.5 104 66 20.0 19.0 Example 22.0 22.0 150 92 25.0 25.5 Example 22.5 20.0 146 91 25.0 22.5 Example 22.5 20.0 146 91 25.0 22.5 Example 22.5 20.0 146 91 25.0 22.5 Example 22.5 20.0 146 89 25.0 22.5 Example 22.5 20.0 146 89 25.0 22.5 Example 22.5 20.0 146 90 25.0 22.5 Example 22.5 20.0 146 88 25.0 22.5 Example 22.5 20.0 146 88 25.0 22.5 Example 22.5 20.0 146 87 25.0 22.5 Example 22.5 20.0 146 89 24.5 22.5 Example 22.0 22.0 150 93 25.5 25.5 Example 22.0 22.0 150 93 25.5 25.5 Table 1 (continued) Carbon fiber woven fabric Average weave Average finenessThicknessWidth density (yarns/cm)(g/m) (mm) W N X W
(cm) Example 20.0 0.018 0.19 0.028 0.56 Example 27.0 0.018 0.22 0.028 0.76 Example 24.0 0.019 0.22 0.028 0.67 Example 25.5 0.018 0.24 0.030 0.77 Example 24.0 0.019 0.22 0.028 0.67 Example 18.0 0.028 0.25 0.040 0.72 Example 26.0 0.017 0.23 0.026 0.68 Example 19.5 0.017 0.18 0.025 0.49 Example 25.5 0.018 0.20 0.037 0.94 Example 24.0 0.019 0.21 - -Example 24.0 0.019 0.20 - -Example 24.0 0.019 0.20 - -Example 24.0 0.019 0.18 - -Example 24.0 0.019 0.17 - -Example 24.0 0.019 0.18 - -Example 24.0 0.019 0.16 - -Example 24.0 0.019 0.15 - -Example 24.0 0.018 0.14 - -Example 24.0 0.019 0.19 - -Example 25.5 0.018 0.24 0.030 0.77 Example 25.5 0.018 0.24 0.030 0.77 Table 1 (continued) Oxidized Carbon fiber fiber woven woven fabric fabric Weave Unit Weave Unit weight density weight density Warp yarnsWeft yarns Warp yarnsWeft yarns (yarns/cm)(yarns/cm)(g/mZ) (9/mz) (yarns/cm)(yarns/cm) Comparative17,0 15.5 213 133 19.0 17.0 Example Comparative- _ - 120 9.0 9.0 Example Comparative22.0 22.0 150 93 25.5 25.5 Example s Table 1 (continued) Carbon fiber woven fabric Average weave Average ThicknessWidth N X W
W
density (yarns/cm)fineness (g/m)(mm) (cm) Comparative 18.0 0.037 0.31 0.050 0.90 Example Comparative 9.0 0.066 0.14 0.104 0.94 Example Comparative 25.5 0.018 0.24 0.030 0.77 Example (Note: In the carbon fiber woven fabrics of Examples 9 and 10 of Table 1, the warp yarns could not be distinguished from weft yarns.) Table 2 Carbon fiber woven fabric Electric Differential Volta a Crush value 9 under resistance pressure in air z compression (m~2cm) permeation (mmAq)at 0.7 A/cm (mm) (V) Example 0.09 9 0.2 0.51 Example 0.10 11 1.8 0.57 Example 0.10 11 0.6 0.60 Example 0.11 10 1.1 0.60 Example 0.11 10 1.1 0.60 Example 0.11 11 1.0 0.55 Example 0.12 11 0.7 0.58 Example 0.07 12 0.2 0.52 Example 0.09 10 1.4 0.58 Example 0.08 10 1.3 -Example 0.07 10 1.4 -Example 0.07 10 1.5 -Example 0.06 10 1.7 -Example 0.05 10 1.9 -Example 0.07 10 - -Example 0.05 10 - -Example 0.05 10 - -Example 0.05 10 - -Example 0.07 10 - -Example 0.11 10 1.1 0.61 Example 0.11 10 1.1 0.62 Table 2 (continued) Carbon fiber woven fabric Electric Differential Volta a Crush value resistance pressure in air z under compression (m ~ cm) permeation (mmAq)at 0.7 A/cm (mm) (V) Comparative0.16 10 2.4 -Example Comparativep,03 8 1.6 0.44 Example Comparative0,11 ~ 10 1.1 0.41 Example Table 3 Press pressureClearance Tensile strength (kg/cm) (Ltm) (kg/cm) Example - - 2.5 Example 50 0 2.6 Example 11 0 2.7 Example 100 0 2.1 Example 150 0 1.7 Example 250 0 1.1 Example 250 150 2.7 Table 4 Number of oxygen atoms/Number of carbon atoms (0/C) Example 0.01 Example 0.11 Example 0.15 Comparative 0.17 Example r INDUSTRIAL APPLICABILITY
Since the carbon fiber woven fabric for a fuel cell of the invention is a thin and dense woven fabric having a small fineness , it can be slightly deformed under compression and is small in the s spaces between the fibers and in undulation. Therefore, it can be suitably used as an electrode diffusion layer to be used in a fuel cell.
Another object of the invention is to provide an electrode element using a carbon fiber woven fabric to be used in a fuel cell of the invention, a fuel cell using the electrode element, and a mobile unit using the fuel cell. A further object of the invention is to provide a method for producing a carbon fiber woven fabric to be used in a fuel cell of the invention.
DISCLOSURE OF THE INVENTION
A carbon fiber woven fabric for a fuel cell of the invention ~s is characterized in that the average fineness of the warp yarns and the weft yarns constituting the woven fabric is in the range of 0.005 to 0. 028 g/m, and that the weave density of the warp yarns and/or the weft yarns is not less than 20 yarns/cm.
It is preferred that the unit weight of the woven fabric zo is in the range of 50 to 150 g/mz .
It is preferred that the thickness of the woven fabric is in the range of 0.1 to 0.3 mm.
It is preferred that the value of N x W is not less than 0 . 6 where N (yarns/cm) is the weave density of the warp yarns and/or zs weft yarns and W (cm/yarn) is the yarn width.
It is preferred that the crush value the woven fabric under compression is not more than 0.15 mm.
It is preferred that the warp yarns and/or the weft yarns are spun yarns.
It is preferred that the electric resistance of the woven s fabric is not more than 30 mS2cm2, and that the differential pressure caused when 14 cm3/cm2/sec of air is passed through the woven fabric in the thickness direction is not more than 5 mm Aq.
It is preferred that the ratio of the number of oxygen atoms to the number of carbon atoms on the carbon fiber surfaces of the woven fabric is not less than 0.06 and less than 0.17.
It is preferred that the woven fabric contains carbon black on its surfaces and/or inside.
It is preferred that the woven fabric contains a water-repellent substance.
~s An electrode element for a fuel cell of the invention is formed of the above-mentioned carbon fiber woven fabric for a fuel cell of the invention.
It is preferred that the electrode element comprises an electrode diffusion layer formed of the above-mentioned carbon Zo fiber woven fabric for a fuel cell of the invention.
It is preferred that the electrode diffusion layer has a catalyst layer disposed thereon in layer.
It is preferred that the electrode diffusion layer has a catalyst layer and a polymer electrolyte film deposited thereon is in layers.
A fuel cell of the invention comprises the above-mentioned electrode element of the invention.
It is preferred that the fuel cell has a grooved separator provided on the electrode element.
A mobile unit of the invention is mounted with the s above-mentioned fuel cell.
A method for producing a carbon fiber woven fabric for a fuel cell of the invention comprises a pressurization step of pressurizing a precursor fiber woven fabric composed of carbon precursor fibers in the thickness direction and a step of carbonizing the precursor fiber woven fabric.
In the method for producing a carbon fiber woven fabric for a fuel cell, it is preferred that the pressurization step is carried out at a heating temperature of not more than 300°C at a pressure of 5 to 500 kg/cm.
~s In the method for producing a carbon fiber woven fabric for a fuel cell, it is preferred that the carbon precursor fibers are oxidized acrylic fibers.
THE BEST MODES FOR CARRYING OUT THE INVENTION
Zo In the carbon fiber woven fabric for a fuel cell of the invention, it is necessary that the average fineness of the warp yarns and the weft yarns constituting the woven fabric is in the range of 0.005 to 0.028 g/m. It is preferable that the average fineness is in the range of 0.01 to 0. 026 g/m, and more preferably zs in the range of 0.013 to 0.022 g/m. An average fineness of more than 0.028 g/m is not preferred, since the woven fabric becomes thick or a space between weaving yarns becomes large.
If the unit weight of a woven fabric is A ( g/m2 ) , the density of warp yarns is Nw (yarns/cm) , and the density of weft yarns is Nf ( yarns / cm ) , then the average f inenes s can be obtained from the s following equation (I).
Average fineness ( g/m ) - A/ ( Nw + Nf ) / 100 ... ( I ) In the carbon fiber woven fabric for a fuel cell of the invention, it is necessary that the weave density of the warp yarns and/or the weft yarns is not less than 20 yarns/cm.
It is preferable that the weave density is not less than 22 yarns/cm. If the weave density is too low, the spaces between weaving yarns become large, and such problems are likely to occur that the catalyst layer is likely to come off , and that since the electrolytic membrane is likely to dry, high cell characteristics ~s cannot be obtained. It is especially preferable that both the warp yarns and the weft yarns have the weave density mentioned above . If the weave density increases , the weaving speed declines to raise the cost. It is, therefore, preferable that the weave density is not more than 35 yarns/cm, and more preferably not more Zo than 30 yarns/cm.
In the measurements of the average fineness and the weave density, in the case where the warp yarns and the weft yarns cannot be identified which is which in the woven fabric, the yarns in a given direction should be considered as warp yarns , and the yarns is in the other direction, as weft yarns.
It is preferred that the unit weight of the carbon fiber woven fabric for a fuel cell of the invention is in the range of 50 to 150 g/m2. A more preferred range is from 70 to 120 g/m2, and a further more preferred range is from 80 to 98 g/m2.
In the case where the unit weight is too low, the spaces s between the weaving yarns constituting the woven fabric are so large that there occur such problems that the catalyst layer comes off and that since the electrolytic membrane is likely to dry, high cell characteristics cannot be obtained. In the case where the unit weight is too high, it is difficult to produce the woven ~o fabric, and the woven fabric tends to be thick. As a result, such problems are likely to occur that the fuel cell is dimensionally greatly changed under pressurization, and that the separator grooves are likely to be filled with the woven fabric. In the case where the woven fabric has carbon black, resin and the like is deposited, the weight excluding these deposits should be the weight of the carbon fiber woven fabric.
It is preferred that the thickness of the carbon fiber woven fabric for a fuel cell of the invention is in the range of 0.1 to 0.3 mm. A more preferred range is from 0.13 to 0.25 mm, and zo a further more preferred range is from 0 . 15 to 0 . 20 . The thickness refers to the thickness measured when a pressure of 0.15 MPa is applied to the carbon fiber woven fabric.
In the case where the thickness is too small , such a problem occurs that since the electrolytic membrane is likely to dry, high zs cell characteristics cannot be obtained. Furthermore, in the case where the thickness is too large, such problems are likely to occur that the fuel cell is dimensionally greatly changed under pressurization, and that the separator grooves are likely to be filled with the woven fabric.
If the weave density of the warp yarns and/or the weft yarns s of the carbon fiber woven fabric for a fuel cell of the invention is N (yarns/cm) and the yarn width is W (cm/yarn), then it is preferred that the value of product N x W is not less than 0.6.
More preferred is not less than 0 . 65 , and further more preferred is not less than 0.7.
The yarn width W refers to the width viewed in the direction perpendicular to the face of the woven fabric. The yarn width W can also be measured with the woven fabric magnified as an SEM
photograph, etc. It is preferred that the N x W values of both the warp yarns and the weft yarns are not less than 0.6 ~s respectively.
In the case where the warp yarns cannot be distinguished from the weft yarns on the woven fabric as explained in the above, the yarns in a given direction should be warp yarns , and the yarns in the other direction, weft yarns.
zo In the case where the value of N x W is too small, there occur such problems that since the spaces between weave yarns are large, the catalyst layer comes off, that since the surface is rough, the contact between the catalyst layer and the separator is not sufficient, and that since the electrolytic membrane is zs likely to dry, high cell characteristics cannot be obtained. It is preferred that the value of N x W is not more than 0.96. More a preferred is not more than 0.90, and further more preferred is not more than 0.85. If the value of N x W is too high, weaving is so difficult as to lower the weaving speed, hence increasing the cost.
s It is preferred that the crush value of the carbon fiber woven fabric for a fuel cell of the invention under compression is not more than 0.15 mm. More preferred is not more than 0.12 mm, and further more preferred is not more than 0.10 mm.
The crush value under compression refers to the difference between the thickness measured at a pressure of 0.15 MPa and the thickness measured at a pressure of 1.5 MPa. In the case where the crush value under compression is too large, there occur such problems that stack clamping is difficult, that it is difficult to achieve a uniform height, and that the woven fabric fills the is separator grooves.
It is preferred that the warp yarns and/or the weft yarns constituting the carbon fiber woven fabric of the invention are spun yarns . Since spun yarns have many voids in them, higher air permeability and higher water permeability can be obtained.
zo It is preferred that the electric resistance of the carbon fiber woven fabric for a fuel cell of the invention is not more than 30 mSZcm2. More preferred is not more than 25 mSZcm2, and further more preferred is not more than 20 m52cm2. If the electric resistance is too high, the woven fabric used in an electrode of zs a fuel cell increases the voltage loss.
The method for measuring electric resistance is as follows .
Two plates each of which is a vitreous carbon plate overlaid with a copper foil, wherein the vitreous carbon plate has the width of 50 mm, length of 200 mm, thickness of 1. 5 mm and a smooth surface, and the copper foil has the width of 50 mm, length of 200 mm and s thickness of 0.1 mm are prepared. The plates are called test electrodes . The two test electrodes are overlaid on each other with the vitreous carbon sheets facing each other, to cross each other at their central portions . The carbon fiber woven fabrics are cut to have area S ( cmz ) , and the cut carbon fiber woven fabrics are pressurized to apply a pressure of 0.98 MPa for the area of the fabrics . At the ends on one side of the two test electrodes , current terminals are installed, and at the ends on the other side, voltage terminals are installed. Using the current terminals, a current of 1 A is made to flow between the two test electrodes.
is The voltage V (V) across the voltage terminals is measured, to calculate resistance R (m52cm2 ) from the following equation ( II ) .
R = 1,OOOV x S ... (II) It is preferred that the differential pressure is not more than 5 mm Aq, when 14 cm3/cm2/sec of air is passed in the thickness Zo direction of the carbon fiber woven fabric for a fuel cell of the invention. A more preferred range is from 0.2 to 2 mm Aq, and a further more preferred range is from 0.4 to 1.5 mm Aq. In the case where the differential pressure is too large, the air permeability, hydrogen permeability and water permeability are is low, and the cell voltage tends to be low. In the case where the differential pressure is too small, the water is likely to evaporate, and the resistance of the membrane tends to be higher.
In the case where carbon black, resin and the like are deposited on the woven fabric, these deposits should be removed before measuring the differential pressure.
s It is preferred that the ratio of the number of oxygen atoms to the number of carbon atoms on the surfaces of the carbon fibers constituting the carbon fiber woven fabric for a fuel cell of the invention is not less than 0.06 and less than 0.17. A more preferred range is not less than 0.10 and not more than 0.16, and a further more preferred range is not less than 0.11 and not more than 0.15.
The ratio ( O/C ) of the number of oxygen atoms to the number of carbon atoms on the surfaces of the carbon fibers constituting the carbon fiber woven fabric is defined by the following ~s equation.
O/C = (Rate of oxygen atoms on fiber surfaces)/(Rate of carbon fibers on fiber surfaces) If the ratio O/C on the surfaces of carbon fibers is less than 0.06, the fiber surfaces are low in hydrophilicity, and the ao migration of water in the yarns owing to the capillary tubes formed by plural carbon fibers tends to decrease . As a result , the extra water in the system cannot be efficiently discharged, and the water produced due to the power generation reaction is accumulated to clog the cathode electrode with water with a tendency of zs lowering the gas diffusibility.
If the ratio O/C on the surfaces of carbon fibers is not less than 0.17, the fiber surfaces become too high in hydrophilicity. Therefore, even in the case where the quantity of produced water is small, the cathode electrode can be clogged with water with a tendency of lowering the gas diffusibility. If s the ratio O/C is in the range mentioned above, the surfaces of the fibers constituting the carbon fiber woven fabric for a fuel cell of the invention are moderately hydrophilic. Therefore, the water can highly migrate in the woven fabric owing to the capillary tubes formed by plural carbon fibers, to give a feature that the cathode electrode is unlikely to be clogged with water. For this reason, the extra water in the system can be efficiently discharged, to allow excellent water control.
The ratio of the number of oxygen atoms to the number of carbon atoms on the surfaces of carbon fibers can be measured by ~s X-ray photoelectron spectroscopy.
It is preferred that the carbon fiber woven fabric for a fuel cell of the invention contains carbon black on its surfaces and/or inside for the purposes of increasing electric conductivity, smoothening the surfaces and controlling the water 2o permeability. The method for adding carbon black is not especially limited, but it is preferred that carbon black is bound to the woven fabric using a resin or the like as an adhesive.
It is preferred that the carbon fiber woven fabric for a fuel cell of the invention contains a water-repellent substance 2s for the purpose of preventing clogging with water when it is used in a fuel cell. Furthermore, a water-repellent substance can also be used as an adhesive for the carbon black. The water-repellent substance is not especially limited, and for example, a fluorine-containing compound, silicon-containing compound or the like can be preferably used.
s The method f or producing the carbon f fiber woven f abric f or a fuel cell of the invention is not especially limited. For example, yarns consisting of carbon fibers can be woven to produce a carbon fiber woven fabric, or carbon precursor fibers can also be woven to produce a precursor fiber woven fabric that is then io carbonized into a carbon fiber woven fabric. As another method, a commercially available precursor fiber woven fabric can also be carbonized to produce a carbon fiber woven fabric. In the case where yarns consisting of carbon fibers are woven, it is likely to occur that the carbon fibers are broken or folded. Furthermore, is the warp yarns and the weft yarns are likely to be shifted to deform the meshes of the produced carbon fiber woven fabric, and the warp yarns and the weft yarns at the edges of the woven fabric are likely to come off . Therefore, the latter method of carbonizing a carbon precursor fiber woven fabric is preferred.
Zo The carbon fibers or precursor fibers of carbon fibers used for producing the carbon fiber woven fabric for a fuel cell of the invention are not especially limited. Examples of them include polyacrylonitrile-based carbon fibers, rayon-based carbon fibers, phenol-based carbon fibers, pitch-based carbon zs fibers, oxidized acrylic fibers, rayon fibers, phenol fibers, infusible pitch fibers, etc. An especially preferred method is to carbonize the woven fabric produced by weaving oxidized acrylic ffibers.
In the process for producing the carbon fiber woven fabric for a fuel cell of the invention, it is preferred to include a s step of pressurizing in the thickness direction, the woven fabric produced by weaving carbon precursor fibers , since the crush value under compression can be kept small, for example, when plural electrode diffusion layers formed of carbon fiber woven fabrics are laminated for producing a fuel cell.
It is preferred that the pressurization in the thickness direction is carried out before or during carbonization. The pressurization before or during carbonization is more effective in lessening the crush value under compression than the pressurization after carbonization.
~s The method of pressurizing before carbonization can be a continuous pressurization method using a roll press or belt press or a surface load pressurization method using a batch press or load. In view of the efficiency of the pressurization step, it is preferred to use a roll press or belt press that allows Zo continuous pressurization.
It is preferred that the temperature during pressurization is not more than 300°C. A more preferred range is from 150 to 250°C, and a further more preferred range is from 170 to 230°C.
In the case where the temperature is too low, the deformation under zs compression is too small, and the effect of reducing the thickness cannot be sufficiently obtained. In the case where oxidized acrylic fibers are used, a remarkable pressurization effect can be observed at 150°C or higher. In the case where the temperature is too high, since the oxidation of carbon precursor fibers in air takes place, the pressurization must be carried out in an s inactive atmosphere. Furthermore, because of high temperature, equipment maintenance and process control become difficult . In the case of oxidized acrylic fibers, the problems of oxidation and deterioration do not occur at 250°C or lower, since the fibers underwent flame-retarding treatment.
In the case where the pressurization is carried out using rolls, it is preferred that the surface of at least one of the two rolls used for pressurization is made of a soft material such as rubber, resin, paper or nonwoven fabric for preventing the breaking of carbon precursor fibers and the decline of tensile is strength. It is preferred that the line load of pressurization is in the range of 10 to 500 kg/cm. A more preferred range is from 50 to 300 kg/cm, and a further more preferred range is from 150 to 200 kg/cm.
In the case where hard rolls made of a metal or the like zo are used for pressurization, it is preferred that a clearance of 50 E,im or more is established or that the line load is kept in the range of 5 to 200 kg/cm, for preventing the destruction of the woven fabric, the breaking of the fibers of the woven fabric, and the decline of tensile strength. A more preferred range of line is load is from 10 to 100 kg/cm, and a further more preferred range is from 20 to 70 kg/cm.
In the case where a surface load is used for pressurization, it is preferred that the pressure is 5 MPa or more.
In the case where a woven fabric of carbon precursor fibers is pressurized while being carbonized, it is only required that s the pressurization is carried out at least at any moment in the carbonization step. In the case where preliminary carbonization at the highest temperature of about 500 to 1,000°C is followed by regular carbonization at the highest temperature of higher than 1, 000°C for carrying out carbonization twice , it is preferred that the woven fabric is pressurized during at least either preliminary carbonization or regular carbonization. The method of pressurization can be a continuous pressurization using rolls or belt, or a surface load pressurization, or a method of carbonizing a rolled woven fabric for pressurization using the tension of ~s rolling and the tension caused by the shrinkage during carbonization, though the method is not limited to these methods.
In the case where a rolled woven fabric of carbon precursor fibers is carbonized, it is preferred that the outermost layer of the roll is covered with paper, film or woven fabric with a Zo surface smoother than the woven fabric, since the woven fabric can be carbonized without wrinkling even at the outermost layer.
More particularly it is preferred to cover the woven fabric of carbon precursor fibers with paper, film or woven fabric made of carbon or any other material capable of being carbonized and is incapable of molten when carbonized, such as a polyimide, cellophane or cellulose.
In the case where a woven fabric of carbon precursor fibers is carbonized and subsequently pressurized, it is preferred to pressurize with the woven fabric wetted with a liquid substance such as water or organic solvent, or to pressurize the woven fabric s having a resin such as a fluorine resin deposited. It is more preferred that a carbonized woven fabric having a resin deposited is pressurized at higher than its melting point or thermal deformation temperature.
In the carbon fiber woven fabric for a fuel cell of the invention, the carbon produced when an organic material deposited on the carbon fibers or carbon precursor fibers is carbonized, can also remain deposited. The deposited carbon has an effect of inhibiting the deformation under the pressurization of the carbon fiber woven fabric, but on the other hand, has a problem ~s of lowering the gas permeability and the flexibility of the woven fabric. Therefore, it is preferred that the amount of the carbon is 20 wt~ or less . More preferred is 5 wt~ or less , and further more preferred is 2 wt~ or less.
The carbon fiber woven fabric for a fuel cell of the Zo invention can be preferably used as an electrode component such as a gas diffusion electrode for a fuel cell, since it has electric conductivity and fluid permeability.
Furthermore, the carbon fiber woven fabric for a fuel cell of the invention can be preferably used as a conductive sheet to zs be used in a fuel cell, especially as an electrode diffusion layer of a fuel cell. It can be especially suitably used as an electrode i7 diffusion layer of a fuel cell having a grooved separator. In the case where a grooved separator is used as passages for feeding oxygen and a fuel to a fuel cell electrode, if the crush value of the carbon fiber woven fabric under compression is large, the s portions of the woven fabric facing the grooves and hence not subjected to compression go into the grooves, to inhibit the function as the passages of oxygen and fuel. The carbon fiber woven fabric for a fuel cell of the invention, that is thin in thickness and small in the crush value under compression, can effectively avoid inhibiting the passage function. As a result, the grooves can have a smaller depth and the device can be made more compact.
Moreover, the carbon fiber woven fabric for a fuel cell of the invention can be preferably used as an electrode diffusion is layer having a catalyst layer disposed thereon as a layer or having a catalyst layer and a polymer electrolyte membrane disposed thereon as layers to form a unit. Still furthermore, the electrode diffusion layer or the unit can be preferably used as a component of a fuel cell. The fuel cell containing the carbon zo fiber woven fabric for a fuel cell of the invention, which is flexible and small in the crush value under compression, is strong against vibration and impact, is compact, and is suitable as a fuel cell for a mobile unit . It is especially suitable as a fuel cell for a mobile unit requiring a compact fuel cell, above all, as for a motor vehicle or two-wheeled car.
Examples are described below. The properties described in 1s the examples were measured according to the following methods.
Crush value under compression:
A carbon fiber woven fabric was placed on a smooth table, and a micrometer indenter having a diameter of 5 mm was allowed s to descend from above. With a load applied to the indenter, the thickness was measured at a pressure of 0.15 MPa, and with the load further increased, the thickness was measured at a pressure of 1.5 MPa. The difference between the thickness measured at a pressure of 0.15 MP and the thickness measured at a pressure of 1.5 MPa was identified as the crush value. A smaller crush value is more desirable.
Electric resistance:
The method described before was used to obtain the electric resistance from the following equation. A lower electric is resistance is more desirable.
R = 1,OOOV x S
where R: Resistance (mS2cmz) V: Voltage across voltage terminals (V) S : Area of carbon f fiber woven fabric ( cmz ) zo Voltage at 0 . 7 A/cmz A carbon fiber woven fabric was coated with a mixture consisting of carbon black and polytetrafluoroethylene, and the coated fabric was heat-treated at 380°C, to produce a woven fabric having a carbon layer. The deposited amount of the mixture zs consisting of carbon black and polytetrafluoroethylene was about 2 mg / cmz .
On the other hand, a mixture consisting of platinum-loaded carbon as a catalyst and Nafion was deposited on both sides of Nafion 112 (produced by E. I. du Pont de Nemours and Company), to prepare a membrane-catalyst sheet . The amount of platinum as s a catalyst was about 0.5 mg/cmz.
The membrane-catalyst sheet was held between two carbon-layered woven fabrics having the carbon layers turned inside, and the laminate was heated at 130°C and pressurized at 3 MPa for integration, to obtain a membrane-electrode assembly io ( MEA ) .
The MEA was held between grooved separators , and the cell characteristicswere measured according to a conventional method.
The cell temperature was 70°C, and the temperature at which hydrogen gas was applied was 80°C , while the temperature at which is air was applied was 60°C. The gas pressure was atmospheric pressure. At 0.7 A/cmz, the hydrogen availability was 70~ and the air availability was 40~ . A higher voltage is more desirable .
At 0.7 A/cmz, 0.5 V or higher is acceptable.
Tensile strength:
zo A woven fabric was cut to have a dimension of 5 to 7 cm in the warp direction and a dimension of 1.5 to 1.7 cm in the weft direction. Several warp yarns at both the edges in the weft direction were removed, to ensure that there were no broken warp yarns in the sample having a length of 5 to 7 cm. The width across zs the remaining warp yarns of the sample was measured as a sample width, and a tensile test was carried out at a span of 3 cm and a tensile speed of 1 mm/min . The value obtained by dividing the maximum load ( kg ) by the sample width ( cm ) was identified as the tensile strength.
Examples 1, 2, 3, 4 and 5 s Spun yarns of oxidized acrylic fibers ("Lastan" produced by Asahi Kasei Corp. , 1/34 Nm = 0.029 g/m) were woven into a plain weave. The woven fabric was carbonized in two steps at the highest temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of each oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness, weaving yarn width W and the value of N x W of each carbon fiber woven fabric are shown in Table 1.
Example 6 ~s Spun yarns of oxidized acrylic fibers (produced by Asahi Kasei Corp. , 1/34 Nm = 0.029 g/m) were used as warp yarns and spun yarns of oxidized acrylic fibers (produced by Asahi Kasei Corp. , 2/34 Nm = 0.059 Nm) were used as weft yarns to produce a plain weave. The woven fabric was carbonized in two steps at the highest 2o temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness , weaving yarn width W and the value of N x W of the carbon 2s fiber woven fabric are shown in Table 1.
Example 7 Oxidized acrylic fibers (produced by Toray Industries, Inc . ) were spun into yarns by a draf t zone system spinning . The fineness of the spun yarns was 1/40 Nm = 0.025 g/m. The spun yarns were woven into a plain weave . The woven fabric was carbonized s in two steps at the highest temperatures of 650°C and 1, 950°C
in an inactive atmosphere, to obtain a carbon fiber woven fabric.
The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight , weave densities , average weave density N, fineness, thickness, weaving yarn width W and the value of N x W of the carbon fiber woven fabric are shown in Table 1.
Example 8 The oxidized acrylic fiber woven fabric of Example 1 was held between carbon sheets , carbonized at the highest temperature of 800°C in an inactive atmosphere with a pressure of 2.8 g/cm2 ~s applied to the woven fabric, depressurized and carbonized at 1,950°C, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness, weaving yarn width W and the value of N x zo W of the carbon fiber woven fabric are shown in Table 1.
Example 9 The oxidized acrylic fiber woven fabric of Example 1 was fed through a roll press consisting of one iron roll and one rubber roll ( iron roll 200°C, rubber roll 120°C ) , to be pressurized at 2s 200 kg/cm. The woven fabric was carbonized in two steps at the highest temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness, weaving yarn width W and the value s of N x W of the carbon fiber woven fabric are shown in Table 1.
Examples 10, 11, 12, 13 and 14 The oxidized acrylic fiber woven fabric of Example 5 was fed through a roll press consisting of two iron rolls ( roll temperature 60 , 100 , 125 , 150 or 200°C ) , to be pressurized at 50 kg/cm. The woven fabric was carbonized at the highest temperature of 1,950°C in vacuum, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness and thickness of each carbon fiber woven ~s fabric are shown in Table 1.
Examples 15, 16, 17 and 18 The oxidized acrylic fiber woven fabric of Example 5 was fed through a roll press consisting of two iron rolls (roll temperature 200°C) , to be pressurized at 11, 100, 150 or 250 kg/cm.
2o The woven fabric was carbonized at the highest temperature of 1,950°C in vacuum, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness and thickness of each carbon fiber woven 2s fabric are shown in Table 1.
Example 19 The oxidized acrylic fiber woven fabric of Example 5 was fed through a roll press consisting of two iron rolls (roll temperature 200°C ) having a clearance of 150 Vim, to be pressurized at 250 kg/cm. The woven fabric was carbonized at the highest s temperature of 1, 950°C in vacuum, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight , weave densities , average weave density N, fineness and thickness of the carbon fiber woven fabric are shown in Table 1.
Example 20 In a beaker containing 500 ml of 0 . 1N sulfuric acid, a carbon sheet was used as the cathode, and the carbon fiber woven fabric of Example 4 cut into a size of 8 cm x 8 cm was used as the anode, for carrying out electrolytic treatment with a current of 48 mA
~s kept flowing for 125 seconds. After completion of electrolytic treatment, the carbon fiber woven fabric was washed with purified water, and dried in a 100°C oven for 10 minutes, to obtain a carbon fiber woven fabric treated to be hydrophilic.
Example 21 zo In a beaker containing 500 ml of 0 . 1N sulfuric acid, a carbon sheet was used as the cathode, and the carbon fiber woven fabric of Example 4 cut into a size of 8 cm x 8 cm was used as the anode, for carrying out electrolytic treatment with a current of 48 mA
kept flowing for 250 seconds . After completion of electrolytic zs treatment, the carbon fiber woven fabric was washed with purified water, and dried in a 100°C oven for 10 minutes , to obtain a carbon fiber woven fabric treated to be hydrophilic.
Comparative Example 1 Spun yarns of oxidized acrylic fibers (produced by Asahi Kasei Corp. , 2/34 Nm = 0.059 g/m) were woven into a plain weave.
s The woven fabric was carbonized in two steps at the highest temperatures of 650°C and 1,950°C in an inactive atmosphere, to obtain a carbon fiber woven fabric. The unit weight and weave densities of the oxidized acrylic fiber woven fabric, and the unit weight, weave densities, average weave density N, fineness, thickness , weaving yarn width W and the value of N x W of the carbon fiber woven fabric are shown in Table 1.
Comparative Example 2 Torayca Cloth (produced by Toray Industries, Inc.) "C06349B" was heated at 1,400°C in an inactive atmosphere, to ~s remove the sizing agent. The unit weight, weave densities, average weave density N, fineness , thickness , weaving yarn width W and the value of N x W of the carbon fiber woven fabric are shown in Table 1.
Comparative Example 3 zo In a beaker containing 500 ml of 0 . 1N sulfuric acid, a carbon sheet was used as the cathode , and the carbon f fiber woven fabric of Example 4 cut into a size of 8 cm x 8 cm was used as the anode, for carrying out electrolytic treatment with a current of 48 mA
kept flowing for 500 seconds . After completion of electrolytic is treatment, the carbon fiber woven fabric was washed with purified water, and dried in a 100°C oven for 10 minutes, to obtain a carbon fiber woven fabric treated to be hydrophilic.
For the carbon fiber woven fabrics obtained in Examples 1 to 21 and Comparative Examples 1 to 3 , the respective values of the crush value under compression, electric resistance, and s differential pressure in air permeation are shown in Table 2, together with the values of the voltage measured with a current of 0.7 A/cmz in the solid polymer electrolyte fuel cells produced using the respective woven fabrics . In the woven fabric of Comparative Example 1, the applied carbon black and polytetrafluoroethylene were separated from the woven fabric, not allow the cell characteristics to be measured.
As can be seen from Tables 1 and 2 , the carbon fiber woven fabrics for a fuel cell of the invention were thin and small in the crush value under compression, showing good cell ~s characteristics. On the other hand, the woven fabrics of Comparative Examples 1 and 2 having an average fineness of more than 0.03 g/m were inferior in cell characteristics. That is, the woven fabric of Comparative Example 1 was relatively thick and large in the crush value under compression. The woven fabric zo of Comparative Example 2 was as low as 0.44 V in voltage.
From the comparison of Examples 5 and 10 to 14, it can be seen that pressing can reduce the thickness, to make the crush value under compression small, and that the effect of thinning at 150°C or higher is remarkable.
zs From the comparison of Examples 5 and 14 through 19 , it can be seen that if the pressure of a roll press consisting of two metallic rolls is raised, the thickness is reduced to make the crush value under compression small. On the other hand, as shown in Table 3, if the pressure is raised especially to 100 kg/cm or higher, it is necessary to establish a clearance between the rolls s and to select an adequate pressure, since otherwise the tensile strength of the woven fabric declines.
As shown in Table 4, since the woven fabrics of Examples 15 and 16 are adequately hydrophilic on the fiber surfaces , their voltages were 0.61 V and 0.62 V respectively, being higher than 0.60 V of Example 4. On the other hand, in Comparative Example 3 , since the ratio O/C was 0 . 17 , the hydrophilicity on the f fiber surfaces was so high that the voltage was as low as 0.41 V.
Table 1 Oxidized Carbon fiber fiber woven woven fabric fabric Weave density weight weight Weave density Warp yarnsWeft yarns Warp yarnsWeft yarns (yarns/cm)(yarns/cm)(g/mZ) (g/mz) (yarns/cm)(yarns/cm) Example 17.0 17.5 104 72 20.0 20.0 Example 24.0 23.0 157 99 28.0 26.0 Example 24.0 17.5 140 88 27.0 20.5 Example 22.0 22.0 150 93 25.5 25.5 Example 22.5 20.0 146 91 25.0 22.5 Example 14.0 18.0 164 102 16.5 20.0 Example 23.0 20.0 126 86 27.0 25.0 Example 17.0 17.5 104 66 20.0 19.0 Example 22.0 22.0 150 92 25.0 25.5 Example 22.5 20.0 146 91 25.0 22.5 Example 22.5 20.0 146 91 25.0 22.5 Example 22.5 20.0 146 91 25.0 22.5 Example 22.5 20.0 146 89 25.0 22.5 Example 22.5 20.0 146 89 25.0 22.5 Example 22.5 20.0 146 90 25.0 22.5 Example 22.5 20.0 146 88 25.0 22.5 Example 22.5 20.0 146 88 25.0 22.5 Example 22.5 20.0 146 87 25.0 22.5 Example 22.5 20.0 146 89 24.5 22.5 Example 22.0 22.0 150 93 25.5 25.5 Example 22.0 22.0 150 93 25.5 25.5 Table 1 (continued) Carbon fiber woven fabric Average weave Average finenessThicknessWidth density (yarns/cm)(g/m) (mm) W N X W
(cm) Example 20.0 0.018 0.19 0.028 0.56 Example 27.0 0.018 0.22 0.028 0.76 Example 24.0 0.019 0.22 0.028 0.67 Example 25.5 0.018 0.24 0.030 0.77 Example 24.0 0.019 0.22 0.028 0.67 Example 18.0 0.028 0.25 0.040 0.72 Example 26.0 0.017 0.23 0.026 0.68 Example 19.5 0.017 0.18 0.025 0.49 Example 25.5 0.018 0.20 0.037 0.94 Example 24.0 0.019 0.21 - -Example 24.0 0.019 0.20 - -Example 24.0 0.019 0.20 - -Example 24.0 0.019 0.18 - -Example 24.0 0.019 0.17 - -Example 24.0 0.019 0.18 - -Example 24.0 0.019 0.16 - -Example 24.0 0.019 0.15 - -Example 24.0 0.018 0.14 - -Example 24.0 0.019 0.19 - -Example 25.5 0.018 0.24 0.030 0.77 Example 25.5 0.018 0.24 0.030 0.77 Table 1 (continued) Oxidized Carbon fiber fiber woven woven fabric fabric Weave Unit Weave Unit weight density weight density Warp yarnsWeft yarns Warp yarnsWeft yarns (yarns/cm)(yarns/cm)(g/mZ) (9/mz) (yarns/cm)(yarns/cm) Comparative17,0 15.5 213 133 19.0 17.0 Example Comparative- _ - 120 9.0 9.0 Example Comparative22.0 22.0 150 93 25.5 25.5 Example s Table 1 (continued) Carbon fiber woven fabric Average weave Average ThicknessWidth N X W
W
density (yarns/cm)fineness (g/m)(mm) (cm) Comparative 18.0 0.037 0.31 0.050 0.90 Example Comparative 9.0 0.066 0.14 0.104 0.94 Example Comparative 25.5 0.018 0.24 0.030 0.77 Example (Note: In the carbon fiber woven fabrics of Examples 9 and 10 of Table 1, the warp yarns could not be distinguished from weft yarns.) Table 2 Carbon fiber woven fabric Electric Differential Volta a Crush value 9 under resistance pressure in air z compression (m~2cm) permeation (mmAq)at 0.7 A/cm (mm) (V) Example 0.09 9 0.2 0.51 Example 0.10 11 1.8 0.57 Example 0.10 11 0.6 0.60 Example 0.11 10 1.1 0.60 Example 0.11 10 1.1 0.60 Example 0.11 11 1.0 0.55 Example 0.12 11 0.7 0.58 Example 0.07 12 0.2 0.52 Example 0.09 10 1.4 0.58 Example 0.08 10 1.3 -Example 0.07 10 1.4 -Example 0.07 10 1.5 -Example 0.06 10 1.7 -Example 0.05 10 1.9 -Example 0.07 10 - -Example 0.05 10 - -Example 0.05 10 - -Example 0.05 10 - -Example 0.07 10 - -Example 0.11 10 1.1 0.61 Example 0.11 10 1.1 0.62 Table 2 (continued) Carbon fiber woven fabric Electric Differential Volta a Crush value resistance pressure in air z under compression (m ~ cm) permeation (mmAq)at 0.7 A/cm (mm) (V) Comparative0.16 10 2.4 -Example Comparativep,03 8 1.6 0.44 Example Comparative0,11 ~ 10 1.1 0.41 Example Table 3 Press pressureClearance Tensile strength (kg/cm) (Ltm) (kg/cm) Example - - 2.5 Example 50 0 2.6 Example 11 0 2.7 Example 100 0 2.1 Example 150 0 1.7 Example 250 0 1.1 Example 250 150 2.7 Table 4 Number of oxygen atoms/Number of carbon atoms (0/C) Example 0.01 Example 0.11 Example 0.15 Comparative 0.17 Example r INDUSTRIAL APPLICABILITY
Since the carbon fiber woven fabric for a fuel cell of the invention is a thin and dense woven fabric having a small fineness , it can be slightly deformed under compression and is small in the s spaces between the fibers and in undulation. Therefore, it can be suitably used as an electrode diffusion layer to be used in a fuel cell.
Claims (20)
1. A carbon fiber woven fabric for a fuel cell, characterized in that the average fineness of the warp yarns and the weft yarns constituting the woven fabric is in the range of 0.005 to 0.028 g/m, and that the weave density of the warp yarns and/or the weft yarns is not less than 20 yarns/cm.
2. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the unit weight of the woven fabric is in the range of 50 to 150 g/m2.
3. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the thickness of the woven fabric is in the range of 0.1 to 0.3 mm.
4. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the value of N x W is not less than 0.6 where N (yarns/cm) is the weave density of the warp yarns and/or the weft yarns and W (cm/yarn) is the yarn width.
5. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the crush value of the woven fabric under compression is not more than 0.15 mm.
6. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the warp yarns and/or the weft yarns are spun yarns.
7. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the electric resistance of the woven fabric is not more than 30 m.OMEGA.cm2, and the differential pressure caused when 14 cm3/cm2/sec of air is passed through the woven fabric in the thickness direction is not more than 5 mm Aq.
8. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the ratio of the number of oxygen atoms to the number of carbon atoms on the carbon fiber surfaces of the woven fabric is not less than 0.06 and less than 0.17.
9. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the woven fabric contains carbon black on its surfaces and/or inside.
10. A carbon fiber woven fabric for a fuel cell, according to claim 1, wherein the woven fabric contains a water-repellent substance.
11. An electrode element for a fuel cell, formed of the carbon fiber woven fabric as set forth in any one of claims 1 through 10.
12. An electrode element for a fuel cell, comprising an electrode diffusion layer formed of the carbon fiber woven fabric as set forth in any one of claims 1 through 10.
13. An electrode element for a fuel cell, according to claim 12, wherein the electrode diffusion layer has a catalyst layer disposed thereon in layer.
14. An electrode element for a fuel cell, according to claim 12, wherein the electrode diffusion layer has a catalyst layer and a polymer electrolyte membrane disposed thereon in layers.
15. A fuel cell comprising the electrode element as set forth in any one of claims 11 through 14.
16. A fuel cell, according to claim 15, wherein a grooved separator is provided on the electrode element.
17. A mobile unit mounted with the fuel cell as set forth in claim 15 or 16.
18. A method for producing a carbon fiber woven fabric for a fuel cell, comprising a pressurization step of pressurizing a precursor fiber woven fabric composed of carbon precursor fibers in the thickness direction, and a step of carbonizing the precursor fiber woven fabric.
19. A method for producing a carbon fiber woven fabric for a fuel cell, according to claim 18, wherein the pressurization step is carried out at a heating temperature of not more than 300°C
at a pressure of 5 to 500 kg/cm.
at a pressure of 5 to 500 kg/cm.
20. A method for producing a carbon fiber woven fabric for a fuel cell, according to claim 18 or 19, wherein the carbon precursor fibers are oxidized acrylic fibers.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001-317813 | 2001-10-16 | ||
| JP2001317813 | 2001-10-16 | ||
| PCT/JP2002/010579 WO2003034519A1 (en) | 2001-10-16 | 2002-10-11 | Fuel cell-use carbon fiber woven fabric, electrode element, fuel cell, mobile unit, and production method for fuel cell-use carbon fiber woven fabric |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2463777A1 true CA2463777A1 (en) | 2003-04-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002463777A Abandoned CA2463777A1 (en) | 2001-10-16 | 2002-10-11 | Fuel cell-use carbon fiber woven fabric, electrode element, fuel cell, mobile unit, and production method for fuel cell-use carbon fiber woven fabric |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20040241078A1 (en) |
| EP (1) | EP1445811A1 (en) |
| JP (1) | JPWO2003034519A1 (en) |
| CA (1) | CA2463777A1 (en) |
| WO (1) | WO2003034519A1 (en) |
Families Citing this family (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7150934B2 (en) | 2002-03-26 | 2006-12-19 | Matsushita Electric Industrial Co., Ltd. | Electrolyte film electrode union, fuel cell containing the same and process for producing them |
| JP4177697B2 (en) * | 2003-04-09 | 2008-11-05 | 松下電器産業株式会社 | Polymer membrane electrode assembly and polymer electrolyte fuel cell |
| JP4333246B2 (en) * | 2003-08-28 | 2009-09-16 | 日産自動車株式会社 | Fuel cell system |
| US20050130018A1 (en) * | 2003-12-15 | 2005-06-16 | Zhiqiang Xu | Fuel cell diffusion layer |
| US7396611B2 (en) * | 2003-12-15 | 2008-07-08 | Plug Power Inc. | Fuel cell catalyst layer |
| EP1827719A4 (en) * | 2004-12-20 | 2009-03-04 | Virginia Polytechnic Inst | DEVICES, SYSTEMS AND METHODS FOR FUEL CELLS |
| CN100521329C (en) | 2005-01-14 | 2009-07-29 | 松下电器产业株式会社 | Stack for fuel cell, and fuel cell |
| US8730877B2 (en) | 2005-06-16 | 2014-05-20 | Qualcomm Incorporated | Pilot and data transmission in a quasi-orthogonal single-carrier frequency division multiple access system |
| TWI296449B (en) * | 2006-01-04 | 2008-05-01 | Univ Feng Chia | Porous carbon electrode substrates and methods for preparing the same |
| TWI352755B (en) * | 2007-07-03 | 2011-11-21 | Univ Feng Chia | Porous carbonized fabric with high efficiency and |
| US9752241B2 (en) | 2012-01-23 | 2017-09-05 | Macdermid Acumen, Inc. | Electrolytic generation of manganese (III) ions in strong sulfuric acid using an improved anode |
| US9534306B2 (en) | 2012-01-23 | 2017-01-03 | Macdermid Acumen, Inc. | Electrolytic generation of manganese (III) ions in strong sulfuric acid |
| US10260000B2 (en) | 2012-01-23 | 2019-04-16 | Macdermid Acumen, Inc. | Etching of plastic using acidic solutions containing trivalent manganese |
| EP2770565A1 (en) * | 2013-02-26 | 2014-08-27 | Vito NV | Method of manufacturing gas diffusion electrodes |
| US10370302B2 (en) | 2014-09-02 | 2019-08-06 | Honeywell International Inc. | Facilitating pitch stabilization in densified carbon fiber preforms |
| US10011535B2 (en) * | 2014-09-02 | 2018-07-03 | Honeywell International Inc. | Sacrificial fibers to create channels in a composite material |
| JP6477401B2 (en) * | 2014-11-04 | 2019-03-06 | 三菱ケミカル株式会社 | Porous electrode substrate, membrane-electrode assembly using the same, and polymer electrolyte fuel cell using the same |
| DE102016224696A1 (en) * | 2016-12-12 | 2018-06-14 | Robert Bosch Gmbh | Bipolar plate for a fuel cell and fuel cell |
| JPWO2019049934A1 (en) * | 2017-09-07 | 2020-10-15 | 東洋紡株式会社 | Gas diffusion layer base material for fuel cells, gas diffusion layer for fuel cells, fuel cells |
| WO2019107241A1 (en) * | 2017-11-29 | 2019-06-06 | 東レ株式会社 | Micro-porous layer and manufacturing method therefor, gas diffusion electrode substrate, and fuel battery |
| WO2020184665A1 (en) * | 2019-03-13 | 2020-09-17 | 東洋紡株式会社 | Carbon electrode material and redox battery |
| WO2020184663A1 (en) * | 2019-03-13 | 2020-09-17 | 東洋紡株式会社 | Carbon electrode material and redox battery |
| WO2020184664A1 (en) * | 2019-03-13 | 2020-09-17 | 東洋紡株式会社 | Carbon electrode material and redox battery provided with same |
| JP2024033106A (en) * | 2022-08-30 | 2024-03-13 | 株式会社不二越 | Carbon fiber fabric for fuel cell gas diffusion layer |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5225120A (en) * | 1975-08-20 | 1977-02-24 | Toyobo Co Ltd | Preparation of active carbon fibers |
| US4293396A (en) * | 1979-09-27 | 1981-10-06 | Prototech Company | Thin carbon-cloth-based electrocatalytic gas diffusion electrodes, and electrochemical cells comprising the same |
| JPS59119680A (en) * | 1982-12-27 | 1984-07-10 | Toyobo Co Ltd | Electrode for flow type electrolytic cell |
| JPS61158669A (en) * | 1984-12-28 | 1986-07-18 | Toray Ind Inc | Electrode plate for bipolar-type fuel cell |
| JP2595519B2 (en) * | 1987-02-16 | 1997-04-02 | 東洋紡績株式会社 | Electrode for liquid flow type electrolytic cell |
| JPH06671B2 (en) * | 1988-09-29 | 1994-01-05 | 王子製紙株式会社 | Highly graphitized porous carbon fiber sheet and method for producing the same |
| JPH09278558A (en) * | 1996-04-09 | 1997-10-28 | Osaka Gas Co Ltd | Carbonaceous porous body and its production |
| JP3773325B2 (en) * | 1997-03-17 | 2006-05-10 | ジャパンゴアテックス株式会社 | Gas diffusion layer material for polymer electrolyte fuel cell and its joined body |
| CA2350925A1 (en) * | 1998-11-16 | 2000-05-25 | Takeji Nakae | Porous conductive sheet and method for producing the same |
| FR2788168A1 (en) * | 1998-12-30 | 2000-07-07 | Messier Bugatti | GAS DIFFUSION ELECTRODE SUPPORTING AN ELECTROCHEMICAL REACTION CATALYST |
| JP2000299113A (en) * | 1999-02-10 | 2000-10-24 | Toray Ind Inc | Conductive sheet and fuel cell electrode substrate using the same |
| WO2000049213A1 (en) * | 1999-02-18 | 2000-08-24 | Showa Denko K. K. | Carbon fiber woven fabric and method for production thereof |
| JP4547754B2 (en) * | 2000-02-10 | 2010-09-22 | 三菱樹脂株式会社 | Pitch-based carbon fiber fabric |
| JP2002203749A (en) * | 2000-12-28 | 2002-07-19 | Daiso Co Ltd | Multilayer electric double layer capacitor |
-
2002
- 2002-10-11 CA CA002463777A patent/CA2463777A1/en not_active Abandoned
- 2002-10-11 US US10/492,798 patent/US20040241078A1/en not_active Abandoned
- 2002-10-11 EP EP02801544A patent/EP1445811A1/en not_active Withdrawn
- 2002-10-11 JP JP2003537140A patent/JPWO2003034519A1/en not_active Withdrawn
- 2002-10-11 WO PCT/JP2002/010579 patent/WO2003034519A1/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| EP1445811A1 (en) | 2004-08-11 |
| WO2003034519A1 (en) | 2003-04-24 |
| JPWO2003034519A1 (en) | 2005-02-03 |
| US20040241078A1 (en) | 2004-12-02 |
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